Gas purification



Nov. 28, 1933. H. A. GOLLMAR GAS PURIFICATION www@ if@ Nw NS q@ Nm* @WNS m Filed March 17, v1931 Patented Nov. 28,

Unirse STATES eArsNroFi-ics i s claims. (or 23-225) My invention relates to the purication ofgas s uch as fuel gas, coke ovengas, water gas, air, orA the like, from hydrogen sulphide contained therein.

. 5 As isrivell known,v fuel gases and various otherA gases contain varying amounts of this noxious impurity which must be more or less completely removed before the gas can be used for many purposes. 1l)

been employed for the puricationof such gas from hydrogen sulphide comprises the process set forth and claimed Y in U. S. Patents No. 1,339,989 to C. J. Ramsburg and No. 1,390,637 to D. L. Jacobson.r This process consistsbriey Vin Washing the gas with an alkaline solution, for example, asolution of sodium carbonate, for-the removal of hydrogen sulphide and other acidic impurities from the gas; The solution 'is then 20; regenerated, for example, byl aeration, heating, or the like, and its, absorbent property with re# spect to hydrogen sulphide being` thereby renewed the solution is then recirculated over the llowing gas.

,According to the specific disclosure ofthe above patents, by far the greater part of the hydrogen sulphide removed from the gas is liberated as suchiin 'the regeneration stage, and the disposal of this noxious material has presentedV a serious 30 problem.

More recently the process described above hasl been somewhatzmodirled by maintaining in the sodiumcarbonate or equivalent solution asubstance or compound hayingthe property of .prei5-venting the liberation of hydrogen sulphidev in the regeneration stage by converting absorbed hydrogen sulphide to materials which are not noxious in character, such as sulphur, sodium thiosulphate, and the like.

or Yanother to employ them. For one thing,

many of the liquids of this character involve the expensive in character, and consequentlyl involve difficulties both by reason of the diiiiculty of maintaining the material in suspension and 5,0 expensive metallic compounds.

Moreover, ltherecovery of sulphur in processes ofevthis character hasA necessarily been accompanied by a removal from the solution of a pory tionof the activeingredients thereof, and more 55 particularly the metalliccompounds, the latter:

One ofthe most successful processes which has While these proof. 40 esses have'in many instances proved entirely sucuse of suspended'metallic compounds relativelyY on account of mechanical losses of the'relatively Y erated as such, the conversion of the lthereby liberated hydrogen sulphide by oxidation into are diiiicult to remove from the sulphur and sometimes may make it diilcultto dispose of the recovered sulphur Without elaborate puricationA n procedures.

On'. the other hand, the employment' or" simple alkaline solutionspsuch as those speciiically set. forth in the above recited patents, have for a disadvantage, aside roin the necessary'liberation of noxious-gas during the actication or regeneration stage, the inability to accomplish a complete purication of gas containing large amountsl of sulphur Without excessive regeneration and other diiiiculties.

It is therefore an object of the present invention toprovide an improvedY process in which a gas may be purified from hydrogen sulphide by means of a solution of the character described hereinabove in, the regeneration of which' at leasty the greater partof the hydrogen sulphide is liberated as such but-in which improved process the liberation of hydrogen sulphide or other noxious material into the atmosphere is avoided.

Asecond object of my invention is to .provide an improved process forpurifying a gas fromV hydrogen sulphide in which a simple A'alkaline solution of the character described hereinabove may be employed for the removal of hydrogen sulphide from the gas, but in which the hydrogen sulphide removed from the gas may be re- 'Y covered in the` form of elemental sulphur Aofl exceptional purity. f

Al further object of .my invention is to provide an improved process for the purification of gas from hydrogen sulphide in which, While simple alkaline solutions are employed for the purification of the gas, a higher degree of purification is accomplished than has heretofore been possible by means A.of such solutions. y

My invention has for further objects such other operative advantages and results as may hereinafter be found to obtain. l

In .the copending application. of F. W. Sperr,

Jr., Serial No. 523,286, iiled March 17, 1931, there is describeda process for the purication ofgas from hydrogen sulphide contained Ytherein Which comprises the treatment of the gas with anabsorbentlliquid capable of regeneration forfurther use and duringV regeneration of which hy drogen sulphide absorbed from said gas is lib` solution capable of being regenerated for further use by treatment of hydrogen sulphide.

Preferably I employ for this purpose a solution of a thiosulphate such as sodium thiosulphate,

ammonium thiosulphate, Zinc thiosulphate, iron thiosulphate or the like, and recirculate the solution through a cycle comprising an absorption stage wherein the solution is brought into contact with the gaseous mixture comprising sulphur dioxide for the absorption of sulphur dioxide therefrom, and a stage wherein the solution is treated with hydrogen sulphide or gases containing the same for the conversion of the absorbed sulphur dioxide to free sulphur andv the restoration of the sulphur dioxide absorbing properties of the solution.

I also prefer to employ the gas to be purified from hydrogen sulphide as a source of hydrogen sulphide for the regeneration of the sulphur dioxide absorbent liquid so that the regeneration of this sulphur dioxide absorbent liquid may constitute an additional purification stage for the removal of hydrogenv sulphide from the liquid treated. This is readily accomplished by locating the stage in which the regeneration of the sulphur dioxide absorbent liquid is accomplished in the path of the gas to be puried with hydrogen sulphide and preferably at a point prior to the passage of the gas through the absorption 'stage of the hydrogen sulphide removal process.

In this manner the degree of purification of the gas from hydrogen sulphide may be considerably increased over Vthe degree of purification' NazCOa -i-HzS :NaI-IS +NaHCO3 As is Well known, the above reaction is reversible and proceeds according to the ratio of the partial pressure of hydrogen sulphide in the atmosphere adjacent to the liquid tothe vapor Apressure of the liquid with respect to hydrogen sulphide. That is to say, that the solution of sodium carbonate broughtinto contact with an atmosphere containing large quantities of hydrogen sulphide will absorb hydrogen sulphide therel from, the above reaction proceeding from left to MYright, whereas if the resultant spent solution is then brought into contact with an atmosphere containing little or no hydrogen sulphide or if the vapor pressure of the` liquid with respect to hydrogen sulphide is increased by heating the 'liquid the reaction reverses itself, proceeding from right to left, and hydrogen sulphide is liberated as such from the liquid.

The term simple alkaline solution as em ployed herein therefore excludes materials con'- taining dissolved or suspended substances in amount sumcient to affect the above v'reaction to such extent as to prevent the liberation of hydrogen sulphide in the manner herein set forth, at least so far as regeneration by heating or aeration is concerned.

With respect to the removal of sulphur dioxide, however, it will be apparent to those skilled in the art that by reason of the fact that the solution which is a simple alkaline solution in the sense indicated, is treated with hydrogen sulphide in one stage andv sulphur dioxide in another, a regeneration takes place which results in the liberation of free sulphur, the reaction being reversed by the chemical reaction of the sulphur dioxide and hydrogen sulphide rather than by a merely physical action.

It will further be apparent that insofar as the recirculation of thiosulphate solution or the like through the hydrogen sulphide and sulphur dioxide absorbing stages is concerned, it is immaterial which of these stages is regarded as the absorption stage and which as the regeneration stage. As a mattei' of fact, each stage accom- 'plishes the absorption of a gas, whether hydrogen sulphide or sulphur dioxide, and each stage also accomplishes a regeneration of the absorbing properties of the solution with respect tothe gas which it encounters in the other stage.

For purposes of uniformity, however, the term absorption stage as employed subsequently in this specification is intended to mean a stage wherein hydrogen sulphide is absorbed from a gas containing it, while the term regeneration stage or actication stage will be employed for the purpose' of designating a stage in which the absorbing properties of a liquid with respect to hydrogen sulphide are restored.

In order that my invention may be fully set forth and understood, I now describe with reference to the accompanying drawing a preferred manner in which it is practiced and embodied. In this drawing,

The single gure is a partially diagrammatic elevational view of apparatus for purifying a gas from hydrogen sulphide according to the invention. i

Referring to the drawing, the removal of hydrogen sulphide from gas to be treated is accomplished in a plurality of vessels comprising a primary absorber l and a secondary absorber 2 and the actication or regeneration of the purifying presentV liquids employed in the absorbers 1 and 2 is acpurined enters thebottom of the primary ab'- 1 sorber l through an inlet 6 and passes upward through the absorber 1 in countercurrent with a descending iiow of a solution of a thiosulphate, for example, a solution of sodium thiosulphate or other liquid, the absorbent properties of which'.4

with respect to hydrogen sulphide are capable of being regenerated by treatment with vsulphur i dioxide. This liquid is introduced to the absorber l through a plurality of sprays 7 or the" like and passes downward in countercurrent with the gas which eventually reaches the top of the tower in a partially purified condition and passes 1,937,193 out of the absorber 1 through a conduit 8 leading tothe bottom of the secondaryv absorber2.'

The spent purifying solution reaching the bottom-of the absorber 1 passes through a conduit 9 to a sulphur-removing device 10, to be described hereinbelow,'and then through a conduit 11 having a pump 12 to the top of the primary actier 3 where it is brought into contact with sulphur dioxide or a gas containing the same obtained in a mannervto be described hereinbelow and passing downward through the actier 3 in countercurrent wth the rising sulphur dioxide is regenerated' for further removal of hydrogen sulphide.`

The regenerated solution then passes from the bottom of the primary actier 3 through a conduit 13 having a pump 14 to the sprays 'l in the top of the primary absorber 1, thus completing its cycle.

' `vlfls stated hereinabove, a sulphur-removing device 10 is preferably provided at one end of the conduit 9 leading from the primary absorber 1. The device 10 may comprise any suitable device for effecting .the `removal of suspended sulphur produced by the reaction between the absorbed hydrogen sulphide and sulphur dioxide, for example, a filter, but in the drawing thereis illustrated a preferred device in which the removal of sulphur from the liquid is accomplished by flotation. v

The preferred device 10 comprises a vessel adapted to contain a body of the liquid 16 and provided with means for agitating or aerating the liquid which in the present instance consists of one or more foraminous tubes `1'7 connected by means of a conduit 13 with a suitable source 19 of air or other gas under pressure. The passage of the air or other gas through the body of solution 16 causes the sulphur to collect in the form of a froth upon the surface of the solution which sulphur froth may readily be removed in the form of a slurry by means of a launder 21 and a conduit 22. f

The partially purified gas leaving theprimary absorber 1 through the conduit 8 passes'to the secondary absorber 2 'where it is treated in countercurrent with an absorbent solution such, for example, as a 1% to 3% solution of sodium carbonate introduced through sprays 23 at the top of the secondary absorber 2.

The purifying solution during its passage down- 'ward through the secondary absorberv 2 removes -reaching the bottom of the secondary absorber 2 passes through a conduit 25 having a pump 26 to the top of the secondary actier 4 and then passes downward through the actier 4 in countercurrent to a rising flow of air or other gas introduced Y from a fan or blower 27 through a conduit '28,

phide.

terminating in the lower portion of the actier 4.

During its passage downward through the actier 4 the solution is regenerated by the action of the air in liberating and removing hydrogen sul- The regenerated or actifled solution reaching the bottom of the actifier 4 is returned through a conduit 30 having a pump 31 to the sprays 23 at the top of the secondary absorber 2, thus completing its cycle, while the actif-ler air reaching the top of the secondary actifier 4 escapes through a conduit 32 provided for that purpose.

While LI have described the actication of the y recirculated sodium carbonate solution by means of air, it will be obvious to those skilled in the art that the actification may be promoted where so desired by heating the solution, or heating alone may be employed foractication in place of aeration.

It will therefore be apparent thatthe air or other gas leaving the top of the secondary actiiler 4 or other regeneration device throughthe conduitA 32 contains a considerable amount of hydrogen sulphide, being in fact equal to the amount of hydrogen sulphide removed in the secondary absorber 2, except for losses due to side reactions which may take place, resulting in the formation of materials incapable of absorbing hydrogen sulphide or of being regenerated merely by heating or aeration.

This gas is then treatedr for the oxidation of the hydrogen sulphide and sulphurv dioxide in any suitable manner, but preferably by contacting thek gas with or without the presence of additional oxygen or fuel, as may be necessary, through a bed of incandescent material.

vIn the instance described, 'where aeration is employed for actiflcation of the solution employed in the secondary absorber 2, the oxidation of hydrogen sulphide to sulphur dioxide does not require the addition of further oxygen as that is ico already containedin the fouled air leaving the secondary actif-ler 4 through the conduit l32. A But where heat alone is employed for actifying the sodiupnr carbonate solution, hydrogen sulphide may be given off in the regenerationstage in the absence of oxygen, and in such instance it may be .neccessary to introduce oxygen to complete oxidaverter Se is also provided at or near Vthe point4 of actiiiei` air introduction with meansv 37 for introducing `fuel such as gaseous or liquid hydrc'carbon or the like. By means of the combustion of such fuel or by any other means, thev bodies 36 are maintained at a high temperature and the hydrogen sulphide and oxygen passing therethrough or thereover react to produce sulphur dioxide, for example, according to the following reaction: l

rThe resultant gases comprising sulphur dioxide are then lead through a conduit 38 to the bottom of the primary actier 3 employed for the purpose of regenerating absorbent liquid employed in the primary actier 3 in the manner described hereinabove andduring which employment the sulphur dioxide contained therein is substantially cernpletely removed so thatA the gases reaching the top of the primary actiiier 3 pass out through a conduit Slprcvided for that purpose in a substantially completely purified condition. It may be pointed out that sulphur dioxide is apparently somewhat less noxious than hydrogen sulphide, or at least .that the release of small duantities'of sulphur dioxide into the atmosphere appears to be less objectionable than the :elease of an equivwith a thiesulphate solution previously treated d with sulphur .dioxide or other solution capable of ner revivicatlon With sulphurA dioxide and to treat thethereby'partly purified gas subsequently with the's'odiuni carbonate'solution or other solution capable of regeneration with air, it will be obvious that the order of these treatments maybe reversed Where so desired. In other Words, the absorber 1 may be located at a point in the path oi' 'the gas being treated subsequent to the position of the absorber 2. The absorber 2 would then become the primary absorber and the absorber 1 the secondary absorber, and the same would apply to the actiiiers 3 and 4.

Certain side reactions which take place in a solution such as a solutionof sodium carbonate ondarysystem. Y

`It will be apparent from the above that my process makes it possible to remove hydrogen sulphide from a gas containing it in a simple and eicacious manner substantially Without liberating noxious gas into the atinosphereand in'which the hydrogen ksulphide removed frein the gas oeing Vtreated is recovered in an extremely pure f orrn,`uncontaininated with such impurities as insoluble metallic compounds.

It Will be apparent to those skilled in the art that the process oi my invention is capable of considerable modification in detail and is therefore not to be liinited to the speciic examples given hereinabove by Way of illustration but. .may variously be practiced and embodied Within "the scope of the claims hereinafter made.

I claim as my invention: 1. The process of purifying a gas from hydrogen sulphide which comprises recirculating an Nalkaline absorbent liquid through a cycle comprising an absorption stage in which the liquid is brought into contact with the gas for the removal of hydrogen sulphide therefroin and a re-Y generation stage wherein hydrogen sulphide absorbed by said liquid from said gas is liberated, removing thereby liberated hydrogen sulphide from said regenerationstage and oxidizing it to sulphur dioxide, Washingthe resultant sulphur dioxide gases with a solution of sodium thiosulphate, removing the resulting solution, regenerating it by subjecting it to Contact With said gas containing hydrogen sulphide, and recirculating it for further washing of said sulphurdoxide gas.

2. The process of purifying a gas from hydrogen sulphide which comprises recirculating an alkaline absorbent liquid through a cycle comprising an absorption stage in which the liquid is brought into contact with the gas for the removal of hydrogen sulphide therefrom, andaregeneration stage wherein hydrogen sulphide absorbed by said liquid from said gas is liberated, removing thereby liberated hydrogen sulphide from said regeneration stage and oxidizingit to sulphur dioxide, Washing the resultant sulphur. dioxide gases with a solution oi sodium thiosulpirate, removing the resulting solution, regenerating it by subjecting it to Contact with saidgas containing hydrogen sulphide at a point prior to said treatment `oi the gas for the removal of said hydrogen sulphide, and recirculating it for fur-` Washing or" said sulphur dioxide gas. 3. The process of purifying a gas containing hydrogen sulphide which comprises subjecting the gas to contact with a solution of sodium carbonate recirculated over a separate regeneration stage wherein hydrogen sulphide absorbed from said gas .isliberated and with a solutioniof av polythi .irate recircuiated ,through a separate regeneration stage, removing hydrogen sulphide liberatedV in the Vregeneration of said sodium ca rbona-te solution, oxidizing it to sulphur dioxide,

andV employing it for .the regeneration of the thiosulphate solution formed from the aforesaid contact of the gas with the solution nate; 

